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Plug flow design

For first order irreversible reaetion at eonstant density A —> produets, (-r ) = kC, the plug flow design equation is... [Pg.369]

For continuous reactors, plug-flow designs require smaller volumes and hence smaller inventories than mixed-flow designs for the same conversion, as discussed in Chapter 5. [Pg.628]

Tilche A., De Poli F., Ercoli L., Tesini O., Cortellini L., Piccinini S. An improved plug-flow design for the anaerobic digestion of dairy cattle waste paper presented to the International Conference State of the art on biogas technology transfer and diffusion , Cairo, November 17-24, 1984. [Pg.386]

Consider a differential section of a fixed bed reactor which is packed with uniform sized catalyst particles. The plug flow design equation for this section is W... [Pg.370]

Before proceeding to Chapter 3, some terms and equations commonly used in reaction engineering need to be defined. We also consider the special case of the plug-flow design equation when the volumetric flow rate is constant. [Pg.45]

Plug-Flow Design Equation at High Mass Flow Rates... [Pg.577]

Plug-flow design equation in differential torm... [Pg.21]

The reaction occurs via a first order free radical chain mechanism. The crack reaction temperature is 500-550 °C, the pressure is mostly kept at 2.0-3.0 MPa. The crack furnace is of plug-flow design with tubes being placed in the convection zone of the furnace, which is equipped with a burner. [Pg.192]


See other pages where Plug flow design is mentioned: [Pg.263]    [Pg.90]    [Pg.267]    [Pg.292]    [Pg.90]    [Pg.76]    [Pg.232]    [Pg.285]    [Pg.92]    [Pg.259]    [Pg.371]    [Pg.147]    [Pg.150]    [Pg.484]    [Pg.263]    [Pg.172]    [Pg.206]    [Pg.354]    [Pg.232]    [Pg.251]    [Pg.163]    [Pg.1739]   


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